Enhanced DOC removal using anion and cation ion exchange resins. (1st January 2016)

• Record Type: Journal Article
• Authors: Arias-Paic, Miguel; Cawley, Kaelin M.; Byg, Steve; Rosario-Ortiz, Fernando L.
• Is Part Of: Water research. Volume 88(2016)
• Page Start: 981
• Page End: 989
• Publication Date: 2016-01-01
• Subjects: Dissolved organic carbon -- Ion exchange -- Hardness removal -- Enhanced removal -- Calcium; Water -- Pollution -- Research -- Periodicals; 363.7394
• DOI: 10.1016/j.watres.2015.11.019
• Languages: English
• ISSNs: 0043-1354

Abstract

Abstract: Hardness and DOC removal in a single ion exchange unit operation allows for less infrastructure, is advantageous for process operation and depending on the water source, could enhance anion exchange resin removal of dissolved organic carbon (DOC). Simultaneous application of cationic (Plus) and anionic (MIEX) ion exchange resin in a single contact vessel was tested at pilot and bench scales, under multiple regeneration cycles. Hardness removal correlated with theoretical predictions; where measured hardness was between 88 and 98% of the predicted value. Comparing bench scale DOC removal of solely treating water with MIEX compared to Plus and MIEX treated water showed an enhanced DOC removal, where removal was increased from 0.5 to 1.25 mg/L for the simultaneous resin application compared to solely applying MIEX resin. A full scale MIEX treatment plant (14.5 MGD) reduced raw water DOC from 13.7 mg/L to 4.90 mg/L in the treated effluent at a bed volume (BV) treatment rate of 800, where a parallel operation of a simultaneous MIEX and Plus resin pilot (10 gpm) measured effluent DOC concentrations of no greater than 3.4 mg/L, even at bed volumes of treatment 37.5% greater than the full scale plant. MIEX effluent compared to simultaneous Plus and MIEX effluent resulted in differences in fluorescence intensity that correlated to decreases in DOC concentration. The simultaneous treatment of Plus and MIEX resin produced water with predominantly microbial character, indicating the enhanced DOC removal was principally due to increased removal of terrestrially derived organic matter. The addition of Plus resin to a process train with MIEX resin allows for one treatment process to remove both DOC and hardness, where a single brine waste stream can be sent to sewer at a full-scale plant, completely removing lime chemical addition and sludge waste disposal for precipitative softening processes. Highlights: Cation and anion exchange demonstrated for pilot and bench scale in a single vessel. Hardness removal correlated with theoretical predictions. Pilot cation and anion resin outperformed anion full-scale plant for DOC removal. Enhanced DOC removal was due to increased removal of terrestrially derived DOC.